film

Incorporating large-particle inorganic cavitating agents in TD shrink films addresses density and opacity challenges, enabling efficient recycling and UV protection by creating large voids, thus achieving low density and high opacity with controlled shrinkage.

WO2025149620A1PCT designated stage expired Publication Date: 2025-07-17INNOVIA FILMS LTD
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Patent Information

Application Number
PCT/EP2025/050547
Authority / Receiving Office
WO · WO
Patent Type
Applications
Current Assignee / Owner
Priority Date
2024-01-11
Filing Date
2025-01-10
Publication Date
2025-07-17

AI Technical Summary

Technical Problem

Existing transverse direction (TD) shrink films face challenges in achieving sufficient cavitation to reduce density for effective recycling, particularly when incorporating opacifying agents like titanium dioxide, which increases density beyond recyclable limits, and struggle with UV protection and opacity requirements.

Method used

Incorporating inorganic cavitating agents with an average particle size greater than 3 microns, primarily calcium carbonate, to create large voids during low strain rate TD orientation, ensuring the film maintains low density and meets opacity and shrinkage requirements.

Benefits of technology

The solution achieves a TD shrink film with a density below 0.95 g/cm³, enabling easy separation in recycling processes, while providing high opacity and UV protection, with shrinkage ratios exceeding 3:1 in the TD to MD direction.

✦ Generated by Eureka AI based on patent content.

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Abstract

The present invention provides a transverse direction shrink film containing an inorganic cavitating agent having an average particle size of greater than 3 microns.
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Description

[0001] FILM

[0002] The present invention concerns a transverse direction shrink film and a method of making said film.

[0003] Transverse direction (TD) shrink films are used to closely wrap polymeric film around an article, for example as a label. These films are more oriented in the transverse direction than in the machine direction and so exhibit a greater shrinkage in the transverse direction than in the machine direction when exposed to elevated temperatures. This means that these films can be loosely placed around an article and then exposed to an elevated temperature to cause shrinkage predominantly in one direction, resulting in the film closely wrapping the article.

[0004] The article that is surrounded by the shrink film is often formed from a different material to the film. Thus, it is important that the two materials can be separated during the recycling process. This is commonly achieved by providing materials with different densities.

[0005] For example, in the case of polyethylene terephthalate (PET) bottles, polyolefin-based TD shrink films can be easily separated from the PET in the recycling process, after shredding, using a sink-float chamber in which PET flakes sink to the bottom and the polyolefin label flakes float to the surface. The end result is a high purity PET recyclate without any ink contamination from the label. There is increasing interest in switching products in both the dairy and home and personal sectors to transparent PET bottle (from HDPE) so that they can be readily recycled in existing PET recycling facilities.

[0006] In many applications, the contents of the article need to be hidden by the label. Additionally, in applications such as in the dairy industry, the label needs to protect the contents from the harmful effects of UV light. In both cases, this requires the use of a full body shrink sleeve that is fully opaque, yet still of a density sufficiently below 1 such that, after printing, the label flakes still float in the recycling process. An opaque label can also enhance any print applied thereto.

[0007] In order to ensure that 99% of the UV region of the electromagnetic spectrum is blocked, without interfering with the near infra-red (NIR) region, a layer of carbon free black can be applied to the label inner surface. However, it is important not to interfere with the NIR region so that the NIR detectors on the recycling lines can see the material of the article through the sleeve, for correct identification and sorting. Thus, the shrink film needs to benefit from a high opacity and whiteness, to either function on its own as an opaque label, or in the case of having a block ink / carbon free black layer on the reverse, to hide the ink layer / carbon free black sufficiently that the label appears white, rather than grey. Opacity and whiteness values of over 75 and 85 respectively are generally accepted as a minimum requirement.

[0008] These levels are easily obtainable simply by adding a sufficient quantity of a pigment such as titanium dioxide (TiOj) to the film structure. However, since TiOj has a density of approximately 4 g / cm3, the density of the final film very quickly exceeds the ideal target of less than 0.95 g / cm3for the finished film, where without any TiOj the density is approximately 0.92 g / cm3. At these densities, separation from other materials such as PET cannot be reliably achieved, as the film does not necessarily float on water.

[0009] Cavitating agents are known in the art to reduce the density of the film, particularly inorganic cavitating agents such as calcium carbonate. The commonly commercially used calcium carbonate is that with average particle sizes of 3 microns or less. These cavitating agents can be used to reduce density to as low as 0.55 g / cm3. However, all other properties of the film must be maintained within workable tolerances, including the shrinkage, tensile properties and coefficient of friction.

[0010] On a typical sequential stenter line, which comprises both a machine direction (MD) orientation step (typically stretching by 3 to 6x the original dimension) followed by a TD orientation step (typically stretching by 5 to lOx the original dimension), generating cavities is relatively easy due to the high strains involved. The cavities are initiated in the very high strain rate MD orientation step and then elongated and grown in the TD orientation step. This creates cavities that are sufficiently large to reduce the density of the film.

[0011] However, in order to obtain the necessary TD shrink properties, TD shrink films are not created using standard sequential stenter stretching and instead, a MD orientation step is often not used at all. If there is a MD orientation step, it is used with a very small draw ratio (typically stretching by 1 to 1.6x the original dimension), which is insufficient to initiate significant cavitation. Thus, the TD shrink sleeve process is almost entirely reliant upon the low strain rate step of the TD orientation to generate cavities, which is very inefficient. It is therefore difficult to create a TD shrink film with good cavitation, particularly the degree of cavitation necessary to have a sufficient impact on the density of the film to compensate for the addition of opacifying agents. It is even more difficult to create a TD shrink film with good cavitation using simultaneous stretching, as cavitation is more difficult to achieve due to the lower strain rate nature of the process in both directions.

[0012] US2004213981 describes a simultaneously oriented polyolefinic film comprising incompatible particles that cause the initiation of voids, where the cast polyolefin is stretched simultaneously in both the MD and TD direction by 8x. This film is therefore a biaxially stretched film, with equal stretching in both the MD and TD directions, and so is not a TD film, even though some TD shrinkage may be seen.

[0013] Thus, there is a need for a TD shrink film having a sufficiently low density to be recovered during a recycling process when it is part of a packaging material containing other polymers.

[0014] According to a first aspect of the present invention, there is provided a transverse direction shrink film containing an inorganic cavitating agent having an average particle size of greater than 3 microns.

[0015] A transverse direction (TD) shrink film is one that is more oriented in the transverse direction than the machine direction. This means that it will undergo more shrinkage in the transverse direction than the machine direction on the application of an elevated temperature.

[0016] The shrinkage in the transverse direction may be more than 3x the shrinkage in the machine direction (MD), or more than 4x the shrinkage in the machine direction, preferably more than 5x the shrinkage in the machine direction. Therefore, the ratio between the TD and MD shrinkage may be more than 3:1, more than 4:1 or more than 5:1.

[0017] This may be created using a draw ratio in the transverse direction of between about 3x and 20x, or between about 5x and lOx and the draw ratio in the machine direction may be between about 0.5x and 3x, or between about lx and 2x. The draw ratio in the transverse direction is therefore significantly higher than that in the machine direction. The film is therefore considered oriented only in the transverse direction, even though a small amount of stretching (and thus shrinkage) may also be seen in the machine direction.

[0018] The amount of shrinkage in the transverse direction may be between about 30 and 95%, may be between about 40 and 90%, may be between about 50 and 85%, as tested using 10 seconds exposure at 95°C in a water bath. The amount of shrinkage in the machine direction may be less than about 20%, less than about 15%, less than about 10%, optionally less than about 6%, as tested using 10 seconds exposure at 95°C.

[0019] The temperature of the annealing rollers during the film stretching process can also affect the degree of MD shrinkage, with an increasing temperature reducing the degree of MD shrinkage. Thus, the temperature of the annealing rollers may be 75°C or greater, preferably 80°C or greater.

[0020] Average particle size in this instance refers to the D50 (i.e. the 50th percentile of the size distribution).

[0021] It has surprisingly been found that using inorganic cavitating agents having a larger average particle size creates sufficiently large voids in TD shrink films. This is unexpected, as TD shrink films have little to no machine direction orientation, and a very low strain rate transverse direction orientation, which does not easily create the necessary voids. However, the present inventors have found that it was only the larger particles out of the natural size distribution that generated any cavities at all, with larger cavities being generated by larger particles.

[0022] Thus, the use of an inorganic cavitating agent with a large particle size removes many of the particles that do not generate voids and ensures that the remaining particles contribute to the cavitation of the film, even under the low strain rate TD orientation step.

[0023] The inorganic cavitating agent may be any suitable cavitating agent known in the art, including calcium carbonate (CaCOs), barium carbonate (BaCOs), aluminium oxide, aluminium sulphate, barium sulphate, magnesium carbonate, silicates such as aluminium silicate (kaolin clay), mica and magnesium silicate (talc), and silicon dioxide, as well as mixtures thereof. The inorganic cavitating agent may be calcium carbonate.

[0024] The inorganic cavitating agent may have an average particle size of greater than 4 microns. The average particle size may be greater than 4.5 microns, optionally greater than 5 microns. The average particle size may be between about 4.5 and 10 microns. It has been found that the larger the average particle size, the greater the degree of cavitation within the film. Thus, the particle size can be tailored to the degree of cavitation and the density desired.

[0025] The D90 (i.e. the 90thpercentile of the size distribution) of the inorganic cavitating agent may be greater than 10pm, optionally greater than 15 pm. The TD shrink film is polymeric and may be a polyolefin-based TD shrink film. By "polyolefin-based" it is meant that the majority of the film by weight is formed from one or more polyolefin. Optionally, more than 75% of the film by weight is formed from one or more polyolefin. The TD shrink film may be a polypropylene-based TD shrink film, in that the majority of the weight of the film is formed from one or more polypropylene-containing polymers. The TD shrink film may comprise a polypropylene / polyethylene / polybutylene terpolymer and / or a polypropylene / polyethylene copolymer.

[0026] The TD shrink film may be a monolayer film or a multilayer film. The TD shrink film may comprise a core layer, one or more intermediate layers and / or one or more outer layers. The TD shrink film may comprise a core layer, an intermediate layer on either side thereof and an outer layer on each of the intermediate layers.

[0027] The outer layers may be printable, sealable, metallised / metallisable and / or barrier layers (either gas or moisture barrier layers). The outer layers may be treated, for example with corona treatment. The outer layers may be printed. The outer layers and / or the intermediate layers are polymeric, may be polyolefinic and may comprise a cyclic olefin copolymer.

[0028] The film may be sealable to itself, so that it can be sealed to form a tube. The seal may be a heat seal or may be produced by solvent welding. This tube can then be placed around an article and exposed to an elevated temperature to cause the film to shrink and closely surround the article.

[0029] The film may comprise one or more conventional additives, including antiblocks, slip components (e.g. wax), tack reducing additives (e.g. fumed silica, silica, silicone gum), UV absorbers, dyes, pigments, colorants, fillers, lubricants, cross-linkers, anti-static agents (cationic, anionic and / or non-ionic, e.g. poly-(oxyethylene) sorbitan monooleate), anti-oxidants (e.g. phosphorous acid, tris (2,4-di-tert-butyl phenyl) ester), gloss improvers, prodegradants, additives to improve ink adhesion and / or printability, additives to increase the coefficient of friction (e.g. silicon carbide), additives to increase stiffness (e.g. hydrocarbon resin), and / or additives to increase shrinkage (e.g. hard resin).

[0030] The core layer may comprise the majority of the thickness of the film. The core layer may comprise more than 60%, optionally more than 70% of the thickness of the film. The inorganic cavitating agent may be located in the core layer of the film. The TD shrink film may comprise between 2 and 15% w / w inorganic cavitating agent, optionally between 4 and 13% w / w inorganic cavitating agent. The film may comprise less than 12% w / w inorganic cavitating agent. The use of larger particle sizes means that less inorganic cavitating agent can be used, as each particle creates a larger cavity or conversely more opacifying agent can be used while still remaining below the density target

[0031] The TD shrink film may comprise an opacifying agent. The opacifying agent may be any opacifying agent conventionally used, including titanium dioxide, aluminium oxide, aluminium sulphate, barium sulphate, calcium carbonate, magnesium carbonate, silicates (aluminium, magnesium), silicon dioxide and combinations thereof. Titanium dioxide may be used due to its very high refractive index.

[0032] The opacifying agent may also act as a pigment and can be chosen to give the desired colour, for example white. Opacifying agents may have an average particle diameter in the range 0.01 to 1 pm, which can provide optimal light scattering (depending on their refractive index). Opacifying agents may have a higher density than the polymer of the film. The cavitation created by the inorganic cavitating agent may offset the increase in density caused by the opacifying agent, thereby retaining the desired density of the film overall.

[0033] The opacifying agent may be in the same layer of the film as the inorganic cavitating agent. This layer may be a core layer of a multilayer film.

[0034] The inorganic cavitating agent and the resulting cavitation may also contribute to the opacity of the film. A component is considered a cavitating agent if it creates a void and an opacifying agent if it contributes to the opacity of the film. Generally speaking, an opacifying agent does not have a particle size great enough to form cavities.

[0035] The TD shrink film may have a thickness of between 20 and 100 microns, optionally between 30 and 80 microns.

[0036] The TD shrink film may have a density of less than 0.95 g / cm3, optionally less than 0.93 g / cm3and optionally less than 0.9 g / cm3before shrinkage. This ensures that, even after printing and shrinkage, the shrink film can be separated from other polymeric materials in a sink-float chamber during a recycling process, as the shrink film will float on water. The TD shrink film may be opaque. The TD shrink film may have an opacity of more than 75, optionally more than 80. The opacity may be measured using the contrast ratio method (for example, using a Diffusion Systems Anglia Opacimeter Model 12). This ensures that the film has the desired optical properties, as well as masking any UV blocking layer (such as a layer of carbon free black) that may be present on one side of the film. The film may block more than 99% of the UV region of the electromagnetic spectrum, without interfering with the near infra-red (NIR) region.

[0037] The TD shrink film may have a whiteness of more than 85. Whiteness can be measured using a spectrophotometer.

[0038] The TD shrink film may have a shrinkage at 95°C (10 seconds in water) of more than 30% in the transverse direction and less than 20% in the machine direction, of more than 40% in the transverse direction and less than 15% in the machine direction, of more than 50% in the transverse direction and less than 10% in the machine direction, optionally more than 60% in the transverse direction and less than 6% in the machine direction.

[0039] The TD shrink film may have a shrinkage at 80°C (10 seconds in water) of more than 25% in the transverse direction and less than 6% in the machine direction, optionally more than 35% in the transverse direction and less than 4% in the machine direction.

[0040] The shrink properties of the film can be adjusted depending on the intended application and the desired properties. The degree of orientation in the machine and transverse directions can be used to alter the shrinkage, as the greater the degree of orientation (caused by a higher stretch ratio and / or lower stretch temperature), the more shrinkage is seen on the application of an elevated temperature.

[0041] The TD shrink film may have a tensile modulus of more than 600 MPa in the machine direction and more than 800 MPa in the transverse direction, optionally more than 700 MPa in the machine direction and more than 1000 MPa in the transverse direction.

[0042] According to a second aspect of the present invention, there is provided a label comprising the TD shrink film discussed above. The label may comprise print on at least one side thereof. The label may have been cut from the TD shrink film discussed above. The label may act as a sleeve, covering the height of the article.

[0043] The label may be printed on both sides thereof. The side intended to be closest to the article may be printed with a UV blocking layer, such as carbon free black. The side intended to be furthest from the article may be printed with wording and / or a pattern.

[0044] The film may be sealed to itself to create a tubular label, which can then be placed around an article before being exposed to an elevated temperature which causes the label to shrink and closely surround the article. The seal may be a heat seal or may be produced by solvent welding.

[0045] According to a third aspect of the present invention, there is provided an article at least partially surrounded by the TD shrink film or label discussed above. By "at least partially surrounded", it is meant that the TD shrink film extends around the perimeter of the article, covering at least part of the article in a continuous manner.

[0046] The article may be entirely surrounded by the TD shrink film. Alternatively, the TD shrink film may create a label that surrounds a part of the article, with other parts exposed. For example, the film may create a tubular label that extends around part of the article, or a sleeve that covers the entire height of the article.

[0047] The article may be a container or other packaging. For example, the article may be a bottle or a jar. The article may comprise a different polymeric material to that in the film. For example, the TD shrink film may be polyolefinic, while the article may be formed from PET or another material.

[0048] TheTD direction of the film may extend around the perimeter of the article (around the circumference of the tubular label). On the application of an elevated temperature, the height of the film does not change but the circumference of the tubular label decreases in order to closely surround the article.

[0049] Thus, the invention provides a way in which to label or decorate an article, using a shrink film that can then be easily separated from the article in a recycling process.

[0050] According to a fourth aspect of the present invention, there is provided a method of making an article discussed above, comprising surrounding at least a portion of the article loosely with the TD shrink film or label discussed above and exposing the TD shrink film or label to an elevated temperature, such that it shrinks in the TD direction in order to closely surround at least a portion of the article. The TD shrink film may be sealed to itself in order to form a tube before being placed around the article. The seal may be a heat seal or may be produced by solvent welding.

[0051] According to a fifth aspect of the present invention, there is provided a method of making a TD shrink film as discussed above comprising including an inorganic cavitating agent having an average particle size of greater than 3 microns in one or more layers of the film and then stretching the film at least 3 times more in the transverse direction than in the machine direction.

[0052] The film may be stretched by between 3 and 20x its original dimension in the transverse direction, optionally between 5 and lOx.

[0053] The film may be stretched by less than 3x its original dimension in the machine direction, optionally less than 1.6x. The film may be stretched lx its original dimension, in that the film may not be stretched at all in the machine direction.

[0054] It has surprisingly been found that even with this low degree of stretching, cavities are still created in the film that can sufficiently reduce the density of the film to compensate for the increase in density caused by any other additives.

[0055] The film may be produced on a stenter. The stretching may be sequential or simultaneous. Alternatively, the film may be produced using a bubble process.

[0056] The film may then be printed on at least one side thereof to form a label. The film may also be sealed to itself to form a tubular label.

[0057] The features of any of the above aspects are equally applicable to any of the other aspects in the present application.

[0058] The invention will now be more particularly described with reference to the following examples.

[0059] Example 1 A variety of five-layer films were created, each comprising two layers of cyclic olefin copolymer on each side of a core layer containing the components outlined in the tables below. The outermost layers on both sides also contained 2500ppm silica antiblock. The films were oriented using a sequential stenter process. The orientation parameters outlined in the tables below were used, in addition to a TD draw ratio of 9.2, followed by a 1.6% relaxation. MDO draw rollers were set to 70°C throughout. As is conventional, the TDO pre-heat zones had a consecutively lower temperature, starting with that in pre-heat zone 1 and finishing at the stretch zone set-point. One side of the film was then corona treated.

[0060] The polypropylene co-polymer elastomer in the films was Vistamaxx 3980FL (ExxonMobil Chemical), while the polypropylene / polyethylene / polybutylene terpolymer in the films was Adsyl 6C (Lyondell Basell). The reclaim film was in-house recycled film (APO type manufactured by Innovia Films), including the same components with the exception of the opacifying and voiding agents.

[0061] Table la

[0062] Table lb

[0063] The properties of the films were then assessed, as outlined in the tables below. Opacity was measured using the contrast ratio method (Diffusion Systems Angla Opacimeter Model 12). Whiteness was measured using an X-Rite Spectrophotometer Ci62 using the CIELab method. Table 2a

[0064] Table 2b

[0065] It was found that the samples that were produced with an MD draw ratio of 1.5x (Table la) had a MD shrinkage of 5% at 95°C. Although the other properties were good, this shrinkage is too high for various applications and so the MD draw ratio was reduced for the later samples (Table lb). For Sample 9, the MD draw ratio was reduced to 1.2 and the MD shrinkage reduced to -1 at 95°C. The remaining samples were therefore made at a MD draw ratio of 1.35x, which achieved an MD shrinkage of 1.5 %. In a later trial (sample 14) it was possible to produce a film with an MD shrinkage of less then 4% at 95°C, with an MD draw ratio of 1.5, by increasing the temperature of the annealing rollers to 80°C.

[0066] Comparing the data from Samples 8, 3, 5, 12 and 13 clearly shows the impact of using larger particles of calcium carbonate, as shown in Table 3 below. This data demonstrates a clear reduction in density with increasing average particle size at TiOj masterbatch concentrations of 15% and 22%. Specifically, the density at 15% TiOj masterbatch decreased from 0.93 g / cm3to 0.873 g / cm3on an increase in average particle size from 3.0 to 4.5 microns, while the density at 22% TiOj masterbatch decreased from 0.93 g / cm3to 0.88 g / cm3on an increase in average particle size from 4.5 to 7 microns.

[0067] Thus, the larger the particle size, the lower the density due to the increased cavitation created. The inclusion of a low level of MD stretching can increase the void initiation and thereby increase the degree of cavitation.

[0068] By calculating the theoretical density of each film without cavitation, a theoretical density reduction factor can also be calculated.

[0069] Table 3

[0070] There is therefore a clear trend of reducing density with increasing particle size, particularly when the impact of MD draw ratio is taken into account.

[0071] The original target specification is met by using calcium carbonate with an average particle size of more than 3.0 microns.

[0072] The change in density of the films was also tested, as a result of the films shrinking. This was achieved by assessing flotation of a selection of the above films in different test solutions and the results are outlined in Table 5 below.

[0073] The shrinkage of the films was tested over a standard range of shrinkage testing temperatures to follow the change in density of the film with different degrees of shrinkage.

[0074] A 25 mm by 25 mm square of the film sample was cut out and immersed in a water bath at a set temperature for 10 seconds (the temperature is noted in Table 5). The sample was then cut into smaller pieces, approximately 5mm by 5mm in size. These pieces were added to a beaker containing the test solution (Table 4) and gently stirred for 2 minutes. The stirring was stopped and the sample was allowed to settle in the solution. The solution was visually observed and it was noted whether the sample had sunk to the bottom of the beaker or whether the sample had floated to the surface.

[0075] If the sample sunk, the result was noted with a and if the sample floated, the result was noted with a "F". The results are summarised in Table 5.

[0076] As film samples will only float on solutions that have a higher density than that of the film sample, this can be used to approximate the density of the film. Additionally, it is often important in recycling processes to have films that float on water, which has a density of 1 g / cm3. Table 4

[0077] The range of test solutions and their specific densities were made using water and isopropyl alcohol, as detailed below.

[0078] Table 5 As can be seen from the results, it was found that as the degree of shrinkage of the film increases (i.e., as the shrinkage temperature increases), the density of the film also increases. Specifically, the increased shrinkage caused by increased temperatures resulted in a density increase of the films such that they float in fewer solutions, i.e. there are fewer solutions having a higher density than the film density after shrinkage.

[0079] This increase can occur fairly sharply, even when exposed to lower shrink temperatures, such as 75°C. For example, when looking at Sample 12, the films sink in all solutions at temperatures over 75°C, due to this sharp increase in density.

[0080] Looking at Sample 3, this film comprises an average CaCOs? particle size of 3 microns and only floated in solutions having a density of 0.96 g / cm3or above (0.98 g / cm3when the shrinkage temperature was 80°C).

[0081] Conversely, Samples 12 and 5 comprise CaCOs with an average particle size of 4.5 microns and floated in solutions as low as 0.9 g / cm3for Sample 5 and 0.94 g / cm3for Sample 12. This therefore demonstrates that the larger particle sizes reduce the density of the film sufficiently that it can float in a variety of solutions, even after shrinkage.

[0082] Samples 13 and 14 comprise CaCOs with an average particle size of 7 microns and also floats in solutions from 0.92 g / cm3upwards for Sample 13 and 0.9 g / cm3for Sample 14.

[0083] This data demonstrates a reduction in starting density when larger particle sizes are present in the film, which means that the films float on more of the test solutions even after shrinkage. This data also demonstrates the importance of having a sufficiently low density before shrinkage, ideally less than 0.95 g / cm3, if not 0.93 g / cm3, to ensure that floatation is still seen on water during a recycling process, even after shrinkage. However, these are not printed films. Thus, in order to account for print on the film, the density needs to be even lower, ideally less than 0.9 g / cm3before printing.

Claims

CLAIMS1. A transverse direction shrink film containing an inorganic cavitating agent having an average particle size of greater than 3 microns.

2. The TD shrink film according to Claim 1, wherein the inorganic cavitating agent is calcium carbonate.

3. The TD shrink film according to Claim 1 or Claim 1, wherein the inorganic cavitating agent has an average particle size of greater than 4 microns, optionally greater than 4.5 microns or greater than 5 microns.

4. The TD shrink film according to any one of Claims 1 to 3, wherein the film is a polyolefin-based TD shrink film, optionally a polypropylene-based TD shrink film.

5. The TD shrink film according to any one of Claims 1 to 4, wherein the film is a multilayer film, which may comprise one or more outer layers and / or one or more intermediate layers.

6. The TD shrink film according to any one of Claims 1 to 5, comprising between 2 and 15% w / w inorganic cavitating agent, optionally between 4 and 13% w / w.

7. The TD shrink film according to any one of Claims 1 to 6, further comprising an opacifying agent, optionally wherein the opacifying agent is titanium dioxide.

8. The TD shrink film according to Claim 7, wherein the opacifying agent is in the same layer of the film as the inorganic cavitating agent, optionally wherein said layer is a core layer of a multilayer film.

9. The TD shrink film according to any one of Claims 1 to 8, wherein the D90 of the inorganic cavitating agent is greater than 10 pm, optionally greater than 15 pm.

10. The TD shrink film according to any one of Claims 1 to 9, wherein the TD shrink film has a thickness of between 20 and 100 microns, optionally between 30 and 80 microns.

11. The TD shrink film according to any one of Claims 1 to 10, wherein the TD shrink film has a density of less than 0.95 g / cm3, optionally less than 0.93 g / cm3and further optionally less than 0.9 g / cm3.

12. The TD shrink film according to any one of Claims 1 to 11, wherein the TD shrink film has an opacity of more than 75, optionally more than 80.

13. The TD shrink film according to any one of Claims 1 to 12, wherein the TD shrink film has a whiteness of more than 85.

14. The TD shrink film according to any one of Claims 1 to 13, wherein the TD shrink film has a shrinkage at 95°C (10 seconds in water) of more than 30% in the transverse direction and less than 20% in the machine direction, of more than 40% in the transverse direction and less than 15% in the machine direction, of more than 50% in the transverse direction and less than 10% in the machine direction, optionally more than 60% in the transverse direction and less than 6% in the machine direction.

15. The TD shrink film according to any one of Claims 1 to 14, wherein the ratio between the TD and MD shrinkage is about 3:1, or about 4:1, or about 5:1.

16. The TD shrink film according to any one of Claims 1 to 15, wherein the TD shrink film has a tensile modulus of more than 600 MPa in the machine direction and more than 800 MPa in the transverse direction, optionally more than 700 MPa in the machine direction and more than 1000 MPa in the transverse direction.

17. A label comprising the TD shrink film according to any one of Claims 1 to 16 and print on at least one side thereof.

18. An article at least partially surrounded by the TD shrink film or label according to any preceding claim.

19. The article of Claim 18, wherein the article is a container or other packaging comprising a different polymeric material to that in the film.

20. A method of making an article according to Claim 18 or Claim 19, comprising surrounding at least a portion of the article loosely with the TD shrink film according to any one of Claims 1to 16 or label of Claim 17 and exposing the TD shrink film or label to an elevated temperature, such that it shrinks in the TD direction in order to closely surround at least a portion of the article.

21. A method of making a TD shrink film according to any one of Claims 1 to 16 comprising including an inorganic cavitating agent having an average particle size of greater than 3 microns in one or more layers of the film and then stretching the film at least 3x more in the transverse direction than in the machine direction.

22. The method of Claim 21, wherein the film is stretched by between 3 and 20x its original dimension in the transverse direction, optionally between 5 and lOx.

23. The method of Claim 21 or 22, wherein the film is stretched by less than 3x its original dimension in the machine direction, optionally less than 1.6x.

24. The method of any one of Claims 21 to 23, wherein the film is produced on a stenter.

Citation Information

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